It is the top section of the distillation column.
The section where the vapour leaves the column to the condenser.
a section above the feed tray called rectifying section and a trays which are above the feed tray called rectifying trays.
- centrifuging - gaseous diffusion - thermal diffusion - electromagnetic separation - expansion from nozzles - laser enrichment - ion exchangers - distillation
Generally: The flooding velocity of the column is the velocity of the vapor rising through the column at which the liquid on each stage is suspended. The flow of vapor up through the column will not allow the liquid to fall down through the column causing the stages to "flood".
Assuming you have binary components the McCabe Thiele Method should be used. Otherwise a process simulator such as Aspen, Pro/II, and/or KGTower should be used.
By flash, it is assumed you mean the amount flashed in the flash zone after entering a column. If the amount flashed is more than you desire, lower the feed temperature. If the feed is some amount of saturated liquid and vapor, you will want to increase the percentage of liquid fed to the column. This applies to a general distillation column with more flash than desired.If this is a crude oil atmospheric distillation column, and you are getting too much kerosene in a side draw, your cut point probably does not meet the required specification. In this case you will need to adjust your pumparound rates and/or increase the amount of reflux.
The rectifying section in a distillation column is where the lighter distillate is being enriched and the heavier components removed. This is in contrast to the stripping section where the lighter components are being "stripped" out of the bottom product and the heavier components consequently concentrated.
distillation column
a section above the feed tray called rectifying section and a trays which are above the feed tray called rectifying trays.
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The fractionation column is used to separate components of a liquid by distillation.
This is an installation used for separation by distillation.
The distillate.
This is a distillation column that doesn't have a continuous feed. The material that is to be distilled will typically be in a round bottom still at the end of the column.
Fractionating column. The process is fractional distillation
i dont know if new improved distillation process have arrived but if you take the old plate distallition or packed column distillation process..then the answer to your question is NO.
If the rate of the distillation through column is too rapid flooding occurs will effect on distillation rate causing low crude column flush zone vaporization that causes low internal reflux rate between GO and GO product and the light materials does not vaporize and it will effect on fractionation ability. Those effects on the specification of the distillation. So effective on crude temp. it will be dropping then crude hydraulic limitation occurred and making the problem worse. so in the top of column boiling film will cause,
it is boiled and ran into a distillation column